US2865940A - Process for preparing saturated aliphatic diisocyanates - Google Patents
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- US2865940A US2865940A US475293A US47529354A US2865940A US 2865940 A US2865940 A US 2865940A US 475293 A US475293 A US 475293A US 47529354 A US47529354 A US 47529354A US 2865940 A US2865940 A US 2865940A
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C263/00—Preparation of derivatives of isocyanic acid
- C07C263/10—Preparation of derivatives of isocyanic acid by reaction of amines with carbonyl halides, e.g. with phosgene
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- This invention relates to novel methods for the prep- It is an object of this invention to provide a practical and effective method for preparing C and C aliphatic diisocyanates from readily available raw materials.
- an: aliphatic conjugated diolefin is treated with finely dispersed sodium or potassium in a selected liquid ether medium and, if desired, in the presence of a relatively small amount of polycyclic aromatic hydrocarbon and/or in the presence of a selected solid, friable, attrition agent at controlled temperatures.
- the reaction products obtained by the selective dimerization reaction are then carbonated at a temperature below C., to give the salts of the dicarboxylic acids.
- the diacids are further reacted, after hydrogenation, with an appropriate nitrogen-containing reactant to yield the desired nitrogen-containing derivatives.
- the diacids can be converted to the di- These dinitril'es are subsequently hydrogenated todiamines.
- the corresponding diisocyanates are prepared by controlled reaction with phosgene.
- butadiene is the aliphatic diolefin starting material
- a mixture of C or C diisocyanates there results from this method a mixture of C or C diisocyanates.
- the diisocyanate products obtained by this synthesis constitute compounds in which the two isocyanate groups (NCO) are separated by 4, 6, 8 or 10 carbon atoms. If some other, higher molecular Weight diolefin is employed in the initial reaction, then the structure of the final products will vary accordingly.
- the above listed specific diisocyanates have been isolated and identified. Compoundsnumbered 2, 3, 5, and 6 are believed, to constitute heretofore unknown compositions. of matter and it is intended to identify them: and claim them assuch.
- the preparation of the 'diisocyanates is carried out by the controlled reaction of phosgene with the corresponding diamines, preferably in the form of their salts such as the hydrochlorides, or the like. In some cases, the carbonates and other salts may be used. Since the diamine dihydrochiorides are generally insoluble, in the preferred liquid reaction media, it is therefore quite desirable to employ these solid salts as finely divided materials in order to achieve reasonable reaction rates.
- the boiling point of the solvent should be sufficiently remote from that of the diisocyanate formed to permit easy and complete separation of the finished product.
- the boiling point of the solvent can be either higher or lower than that of the particular diisocyanate concerned.
- the use of inert solvents with high boiling points is desirable because the reaction time is considerably shortened thereby. This greatly diminishes the possibilities of self-polymerization of the diisocyanate molecules from long contact of the products at high temperatures.
- the reaction of phosgene with diamine dihydrochloride must of necessity be carried out in solvents inert to the active hydrochloric acid gas, phosgene and diisocyanates.
- hydrocarbons such as benzene, toluene and xylene have been used in those cases where the resultant carbonyl chlorides are sufiiciently unstable at the boiling point of these solvents.
- chlorobenzcne and o-dichlorobenzene or the higher alkylated benzenes such as t-butylbenzene or secondary amylbenzene are very effective.
- the precise choice of a solvent for any particular reaction depends on several factors including the type of diamine to be converted, the boiling point of the resultant diisocyanate, and the method of isolation to be used, e. g., crystallization or distillation.
- the diisocyanates are isolated from the reaction mixture by first removing traces of hydrochloric acid and unreacted phosgene by gentle boiling with nitrogen purging. Distillation under reduced pressure generally removes the solvent first and the residue may then be distilled to any degree of purity. In some cases the diisocyanate may boil lower than the inert solvent used in which case conditions are arranged to take advantage of this. Under certain conditions, the reaction product (diisocyanate) need not be isolated as such but can be reacted directly in the inert solvent with alcohols, glycols, amines, etc., and the end product isolated by appropriate means.
- diisocyanates are of wide usage in chemical synthesis. They are especially useful in the preparation of polymeric materials. Other ways in which they are utilized include as blowing agents in plastics, in preparations of synthetic rubbers, as cross-linking compounds for polyester, polyamide, and polyesteramide rubbers, as adhesive intermediates, and as chemical intermediates for the preparation of polyurethanes.
- EXAMPLE I based on the butadiene used) of para-terphenyl and 69 parts of sodium dispersed in 69 parts of isooctane.
- the average particle size of the sodium was 15 microns.
- a stream of gaseous butadiene amounting to a total of 168 parts was passed into the reactor over a 4-hour period while maintaining vigorous agitation and a reaction temperature at about 25 C. During this period the disodium derivatives of the C formed.
- this dimerization reaction was carried out in a ball mill as the attrition type apparatus using sodium chloride as the solid, friable attrition agent.
- the results and products were substantially the same as those obtained above, except that a faster reaction rate and a somewhat higher yield are obtained.
- reaction mixture containing the disodium derivatives as a slurry was carbonated by contacting it with an excess of solid carbon dioxide. After evaporation of excess CO dimethyl ether and isooctane, a solid product consisting essentially of the sodium salts of the C unsaturated dicarboxylic acids remained. An alkaline solution of the dicarboxylic acids was hydrogenated using a nickel catalyst.
- the hydrogenated diacids thus obtained were precipitated by addition of mineral acid.
- the combined yield of IO-carbon atom diacids was 87% based on the sodium.
- the mixed diacids are essentially composed of sebacic acid, a,a-diethyladipic acid, and u-ethylsuberic acid in the approximate ratio of 4:1:5.
- These dibasic acids may be separated by any of a number of procedures involving extraction, recrystallization or distillation. For example, the entire mixture may be esterified, fractionally distilled, and the resultant diester fractions then hydrolyzed. By such a procedure the above reaction product yielded the following fractions:
- butadiene dimers were rrecovery -of 1,6-diaminooctane.
- the ether extract was then heated to remove solvent and the product distilled under reduced pressure for the .
- The-,yield was-100 parts ;of 1 ,-6-diaminooctane; B. P. 75 Cflat I mmuHgpressure.
- reaction mixture was refluxed for 30 minutes, then cooled and filtered. There was: recovered-6 parts of unreacted diamine. Continuous ether extraction for 16 hours gave, after solvent removal and distillation at 2 "mm. Hg, '55partsof 3,6-diaminooctane; 8134%*yield; "-B. P. 60C.
- EXAMPIJEIV 5 8.5. :parts of the; dihydrochloride of. 3,6.-.diaminooctane :were suspended vin about 5 500-1parts .by volume of xylene .;;and:subjectednto the action-ofphosgene at C. for 524 r hours.
- EXAMPLE VI The dihydrochloride of 2,5-diethyl-1,6-diaminohexane (24.5 parts) was suspended in 400 parts of dry xylene and raised to reflux temperature. A slow stream of phosgene was passed through the stirred suspension for 5 hours, during which time the reaction mixture became homogeneous. The preparation was distilled at atmospheric pressure to remove xylene and at 2 mm. pressure at which the 2,5-diethyl-1,6-diisocyanohexane was obtained as a water white liquid (B. P. 95-96 C.) in 55% yield, 11.3 gms.
- the method of preparing saturated aliphatic C diisocyanates in which the isocyano (NCO) groups are separated by at least 4 carbon atoms which includes the steps of dimerizing butadiene in the presence of sodium in finely dispersed form in an active ether diluent and in the presence of at least one dimerization activator, immediately carbonating the resulting organornetallic diene intermediate, neutralizing the resulting dialkali metal salts of dicarboxylic acids to obtain the free diacids, hydrogenating the unsaturated diacids, reacting the saturated diacids with at least one ammonia releasing agent to obtain the diamides, treating the diamides with alkaline hypohalite to give the diamines, and reacting the diamines with phosgene to obtain the C diisocyanates.
- the method of preparing saturated aliphatic C diisocyanates in which the isocyano (NCO) groups are separated by at least 6 carbon atoms which includes the steps of dimerizing butadiene in the presence of sodium in finely dispersed form in an active ether diluent and in the presence of at least one dimerization activator, immediately carbonating the resulting organometallic diene intermediate, neutralizing the resulting dialkali metal salts of dicarboxylic acids to obtain the free diacids, hydrogenating the unsaturated diacids, heating the saturated diacids with at least one ammonia releasing agent to obtain the dinitriles, hydrogenating the resulting dinitriles to diamines, and reacting the diamines with phosgene to obtain the C diisocyanates.
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Description
2 Claims. (Cl. 2604'53) This invention relates to novel methods for the prep- It is an object of this invention to provide a practical and effective method for preparing C and C aliphatic diisocyanates from readily available raw materials.
Itis a further object to selectively react butadiene to react the resulting diacid products with. suitable reagents toform C and C diamines and convert these diamines to the corresponding diisocyanates by reaction with phosgene.
It is a more particular object of this invention to selectively dlmerize 1,3-butadiene using finely dispersed corresponding diisocyanates.
Initially, an: aliphatic conjugated diolefin is treated with finely dispersed sodium or potassium in a selected liquid ether medium and, if desired, in the presence of a relatively small amount of polycyclic aromatic hydrocarbon and/or in the presence of a selected solid, friable, attrition agent at controlled temperatures. The reaction products obtained by the selective dimerization reaction are then carbonated at a temperature below C., to give the salts of the dicarboxylic acids. The diacids are further reacted, after hydrogenation, with an appropriate nitrogen-containing reactant to yield the desired nitrogen-containing derivatives.
For example, the diacids can be converted to the di- These dinitril'es are subsequently hydrogenated todiamines.
From the diamines, the corresponding diisocyanates are prepared by controlled reaction with phosgene.
If butadiene is the aliphatic diolefin starting material, there results from this method a mixture of C or C diisocyanates. The diisocyanate products obtained by this synthesis constitute compounds in which the two isocyanate groups (NCO) are separated by 4, 6, 8 or 10 carbon atoms. If some other, higher molecular Weight diolefin is employed in the initial reaction, then the structure of the final products will vary accordingly.
The generalized formula for these C and C diisocyanates is as follows:
tates atent fiice 2,865,940 Patented" Dec. 23, 1.9.58
Using: the: outlined series of reactions and starting with. but-adiene, a number of diisocyanates were prepared from sebacic acid, a-ethylsuberic acid, and. a,u-.diethyladipic acid- The. specific diisocyanate compounds prepared are those corresponding to the following formulas: (.1) OCNCH CH CH CH CH CH CH CH -NCO 1,8-diisocyanooctane (-2) OCNCH2CH2CHzCH2CH2CHCH2CH3 N 00- 1,6;diisocyanooctane (3) OH-sCHrClHCHzCHzCHCHzCHa N 0.0 N O O 3,6-dii's0cyanooctaue- (-l) 0CNCH CHzCHrCHzCHzCHzCHLaCH2CH2CH NCO lid-diisocyanodeeaue 2,5-dietl1yl-l,6=diisocyanol1exane The above listed specific diisocyanates have been isolated and identified. Compoundsnumbered 2, 3, 5, and 6 are believed, to constitute heretofore unknown compositions. of matter and it is intended to identify them: and claim them assuch.
Mixtures of C diisocyanates comprising essentially compounds above numbered 1, 2, and 3 are obtained by a process hereln described. Mixtures of C diisocyanates comprising essentially compounds above numbered as 4, 5, and 6 are also obtained by a process herein described.
The preparation of the 'diisocyanates is carried out by the controlled reaction of phosgene with the corresponding diamines, preferably in the form of their salts such as the hydrochlorides, or the like. In some cases, the carbonates and other salts may be used. Since the diamine dihydrochiorides are generally insoluble, in the preferred liquid reaction media, it is therefore quite desirable to employ these solid salts as finely divided materials in order to achieve reasonable reaction rates.
Incarrying out the reaction of the diamines or their equivalent salts, with phosgene, it is generally necessary to employ elevated temperatures. If desired, the amine salts can be reacted with phosgene at temperatures upto. 250300 C. This forms intermediate carbamylchl'orides which are then decomposed with a base, for example, lime.
It is preferred, however, to use relatively high boiling, inert solvents as media for the reaction. This technique avoids the use of lime for decomposition.
Since completion of the reaction to obtain the diisocyanates depend cnthe decomposition of the intermediate carbamyl chlorides, there must'be used an inert solvent with a boiling point high enough to accomplish this.
The boiling point of the solvent, however, should be sufficiently remote from that of the diisocyanate formed to permit easy and complete separation of the finished product. Thus the boiling point of the solvent can be either higher or lower than that of the particular diisocyanate concerned. The use of inert solvents with high boiling points is desirable because the reaction time is considerably shortened thereby. This greatly diminishes the possibilities of self-polymerization of the diisocyanate molecules from long contact of the products at high temperatures.
The reaction of phosgene with diamine dihydrochloride must of necessity be carried out in solvents inert to the active hydrochloric acid gas, phosgene and diisocyanates. For this purpose hydrocarbons such as benzene, toluene and xylene have been used in those cases where the resultant carbonyl chlorides are sufiiciently unstable at the boiling point of these solvents. Where still higher decomposition temperatures are required, chlorobenzcne and o-dichlorobenzene or the higher alkylated benzenes such as t-butylbenzene or secondary amylbenzene are very effective. The precise choice of a solvent for any particular reaction depends on several factors including the type of diamine to be converted, the boiling point of the resultant diisocyanate, and the method of isolation to be used, e. g., crystallization or distillation.
Generally, the diisocyanates are isolated from the reaction mixture by first removing traces of hydrochloric acid and unreacted phosgene by gentle boiling with nitrogen purging. Distillation under reduced pressure generally removes the solvent first and the residue may then be distilled to any degree of purity. In some cases the diisocyanate may boil lower than the inert solvent used in which case conditions are arranged to take advantage of this. Under certain conditions, the reaction product (diisocyanate) need not be isolated as such but can be reacted directly in the inert solvent with alcohols, glycols, amines, etc., and the end product isolated by appropriate means.
These reactions may be carried out either in a batchwise or in a continuous manner and it is not intended to limit the process to any particular method of operation.
The herein described diisocyanates are of wide usage in chemical synthesis. They are especially useful in the preparation of polymeric materials. Other ways in which they are utilized include as blowing agents in plastics, in preparations of synthetic rubbers, as cross-linking compounds for polyester, polyamide, and polyesteramide rubbers, as adhesive intermediates, and as chemical intermediates for the preparation of polyurethanes.
The more detailed practice of the invention is illustrated by the following examples, wherein parts are given by weight unless otherwise specified. These examples and embodiments are illustrative only, and the invention is not in any way intended to be limited specifically thereto except as indicated by the appended claims.
EXAMPLE I based on the butadiene used) of para-terphenyl and 69 parts of sodium dispersed in 69 parts of isooctane. The average particle size of the sodium was 15 microns. A stream of gaseous butadiene amounting to a total of 168 parts was passed into the reactor over a 4-hour period while maintaining vigorous agitation and a reaction temperature at about 25 C. During this period the disodium derivatives of the C formed.
Alternatively, this dimerization reaction was carried out in a ball mill as the attrition type apparatus using sodium chloride as the solid, friable attrition agent. The results and products were substantially the same as those obtained above, except that a faster reaction rate and a somewhat higher yield are obtained.
In either case, the reaction mixture containing the disodium derivatives as a slurry was carbonated by contacting it with an excess of solid carbon dioxide. After evaporation of excess CO dimethyl ether and isooctane, a solid product consisting essentially of the sodium salts of the C unsaturated dicarboxylic acids remained. An alkaline solution of the dicarboxylic acids was hydrogenated using a nickel catalyst.
The hydrogenated diacids thus obtained were precipitated by addition of mineral acid. The combined yield of IO-carbon atom diacids was 87% based on the sodium. The mixed diacids are essentially composed of sebacic acid, a,a-diethyladipic acid, and u-ethylsuberic acid in the approximate ratio of 4:1:5. These dibasic acids may be separated by any of a number of procedures involving extraction, recrystallization or distillation. For example, the entire mixture may be esterified, fractionally distilled, and the resultant diester fractions then hydrolyzed. By such a procedure the above reaction product yielded the following fractions:
I. 26 parts a,u-diethyladipic acid II. 131 parts a-ethylsuberic acid III. 87 parts sebacic acid Sebacic acid obtained as fraction III above (1010 parts) was placed into a three necked reaction flask fitted with gas inlet tube, stirrer, and vapor outlet leading to a water cooled condenser. The vapor outlet was arranged to permit the insertion of a thermometer directly into the flask. This flask was heated in an oil bath whose temperature was controlled by suitable electronic equipment actuated by the mercury column in the thermometer.
Heat was applied and dry ammonia gas introduced when the temperature reached C. The temperature was permitted to rise to about 200 to 220 C. at which point it was held constant and the gas (NH fiow maintained for from 7 to 15 hours depending on the conversion desired. About 30 parts of H 0 was obtained per mole of acid.
When enough water was collected to indicate the desired level of conversion, the molten charge was poured into flat metal pans which caused the crude amide to solidify in a few minutes. This solid was then comminuted to about 20 mesh and extracted for several hours with 2% sodium hydroxide solution. Filtration, followed by washing with methanol resulted, after drying, in the isolation of pure sebacamide, M. P. 210-212 C. in about 80% yield.
In another experiment, 360 parts of li-eihyi suberic acid, fraction II, was reacted with NH gas at 220 C. in the manner described above. After purification by leaching with excess N/2 alkali and washing with methanol, 177 parts of the diamide was obtained; M. P., 0; yield, 49.6%.
In a third experiment, 202 parts of pure a,m'-diethyladipic acid (mixture of racemic and meso forms) prepared and isolated as fraction 1, was treated with NI-I gas at 200220 C. for 7 hours. The reaction product was finely ground and treated with aqueous ammonia to remove acidic material, both unreacted and side reaction products. The ammonia insoluble diamide was washed with distilled water to remove all traces of ammonia. A final wash with methanol followed by air drying, gave 102 parts of pure diamide; 50% yield, melting range 235-270 C. (mixture of racemic and meso forms).
butadiene dimers were rrecovery -of 1,6-diaminooctane.
..To. prepare.1, 8-diaminooctane, sebaeamide obtained. as .describedabove was .used. directly. Into .a' reaction flask equipped with etficient stirring,..p1:ovision'for temperature nda thermometer was. placed asolution of'4'52 -parts (11.3 moles) of sodiumhydroxide (40% excess) .in 900,.parts of waterand .l200..parts ice. "Bromine (352 .parts, 2.2 moles) was added .dropwise with vigorous stirring at such a rate that littleif any. free bromine was present at anytime.
The temperature. of the hypobromite solution was then raised to about 151C. and12 00 parts (.lmole) of'finely powdered sebacamide was addedas rapidly as, possible. .-After..the.a ddition ofsebacamide, the. temperature o'f'the .reaction mixture rose graduallywith 'the solution of all .=su spended matter. .Theffinal.reactiontemperature was about 60-65 C. "Cooling,.followed by continuous liquidliquid extraction with ethyl ether,jgave, after 8 hours, .a yield. of71.5.parts.of 1,8-diaminooctane;'50% yield; QB. 'P..-94 C. at 1 mm. Hg. pressure. 'lThe amine can be isolated as the carbonate ordihydrochloride, if desired.
'.In another experiment, 177 parts of a-ethyl suberaznide wasaddedto a'cold aqueous solution of (2000 parts) con- ;taining 326.4:parts bromine and 400 parts sodium hydroxide at 5 C. .The. reaction proceeded rapidly with the reaction mixture reaching a temperature of 75C. in 130 minutes. After refluxing'for'l hour, the. clear solution was subjected to continuous extraction with ether for 48 hours.
The ether extract was then heated to remove solvent and the product distilled under reduced pressure for the .The-,yield was-100 parts ;of 1 ,-6-diaminooctane; B. P. 75 Cflat I mmuHgpressure.
Into a reaction flask provided with stirrer, dropping funnel and thermometer, was introduced 226 parts (5.7 moles) sodium hydroxide dissolved in 450 parts water. A cold slurry of this alkali solution wasmade byadding 600 parts of crushed ice. To this slurry at -I2 .C., was added 176 parts (1.1 mole) liquid bromine. To the freshly prepared solution of cold hypobromite was then added 100 parts (0.5 mole) of the diamideof egosdiethyladipic acid. After minutes,;the temperature was permitted to rise to C. spontaneously.
The reaction mixture was refluxed for 30 minutes, then cooled and filtered. There was: recovered-6 parts of unreacted diamine. Continuous ether extraction for 16 hours gave, after solvent removal and distillation at 2 "mm. Hg, '55partsof 3,6-diaminooctane; 8134%*yield; "-B. P. 60C.
Into a reaction flask fitted with-reflux condenser-and gasinlet was placed partsoffinely dividedhydrochloride ofI1,8-diaminooctane made as described above-uand about 400 parts by volume of sec-amyl benzene. At reflux temperature (187 C.) a slow stream of phosgene "was maintaineduntil all solid suspensionhas disappeared. This required 2 to 3 hours.
Nitrogen was passed through the hot solution to remove hydrochloric acid and phosgene gas. Fractional distillation removed the sec-amyl benzene solvent which can be reused. At 97 to 105 C. and 0.1 mm. Hg, a fraction of 34.0 parts of diisocyanate was obtained; yield EXAMPLE II chloride of 1,8-diaminooctane and about 400 parts by volume of dry xylene. At reflux temperature, phosgene was introduced and continuously added for 7 hours.
unconverted dihydrochloride. This indicated a conversion of diamine to diisocyanate of 76.2%. Distillation resulted in the recovery of 34.5 parts of corresponding diisocyanate boiling between 98-104 C. at 0-1 mm. Hg. This was a 76.8% yield.
icondenser and 'about hydrochloric .acidzvgas was added 'sto -converti;this to.'.the zdihydrochloride.
J-trme.
f:Hg;' yield 93.5. o'f 3,6-diisocyanooctane. i the :cQrrespOn'ding .Idimethylt urethane (M.
4 basic acid' is relatively insoluble.
" end of this time, 1C. Fforf127: minutes. reaction vessel at .6 I "'EXAMPLE'ZIII Into a "reaction :xflask fitted with 5. gas ii-nlet rand reflux was uplaced 57:5 zparts L'Of :1; diaminooctane 700 .parts .by volume of; xylene. IiSuflicient dry Heat was then applied-andlthe'mixture'grefluxed. Phos- .:gene=gas was introduced through adispersion. tube-I for 72 .i'hours.
:carbon and xylener solutioni'filtered. :Fractionationat The'homogeneous reaction mixture was boiled to: remove dissolvedtphosgene, .decolorized with activated of. L,6-7d-iisocyanooctane; C.w.at 0.1 mm. Hg; %;yield. A sample of this diisocyanate was convertedsto the=methyla1rethane, M. P. 85.5-86 C. andassuch. gave the following analyses: Calculated for C 'H ;O4N C, 55.36; H, 9.29; N, 10.76; found-C,55i29; H, 9:35; 'N,i 10.73.
. EXAMPIJEIV :5 8.5. :parts of the; dihydrochloride of. 3,6.-.diaminooctane :were suspended vin about 5 500-1parts .by volume of xylene .;;and:subjectednto the action-ofphosgene at C. for 524 r hours.
The reaction; 'mix-tureflbecame:homogeneous rafter that Removal'of solventpand distillation at .ireduced pressure gave 49.4 parts; B. P. 66-70.C.:-at 0.5 mm. .Analysis of -P. 154
results: Calculated for +9.29; .--N, 210.76; foundC,
gave the following EXAMPLE *V The diamin'es and diamine salts used as starting matealspforrthe reactions to, .produce C diisocyanates of Examples V and VI wereprepared by the following method.
A mixture of hydrogenated C diacids consisting essentially of sebacic acid, a,m'-diethylad ipic acid .and a-ethylsuberic acid was obtained as described in .the .introduction.tosExample- I.
These saturated mixed C diacids'wereextracted with benzene to 'dissolve the branched-chainacids. '=.The.;se- The branched-chain of the C acids (a-ethylsuberic, acids, in the ratio of'?8: 1:1,
'for about 56 /2. hours at a temperature'of..160:C. -At the the. temperature was increased: to 220 The products. were .distilled from the :atmospheric pressure until no imore distillate was ;obtained, .themaximum temperature being 340 C.
.The :dist'illate' was taken .up :irv excess diethyl zether and extracted with carbon atom dinitriles distilled under reduced pressure.
boiling at about ISO- C./10 mm. gave 57 parts (58% yield) of the mixed dinitriles. Fractionation of this mixture gave 6 parts of a,a-diethyladiponitrile, 36 parts of a-ethylsuberonitrile and 6 parts of sebaconitrile boiling at -198 C./15 mm., a,a'-diethyladiponitrile boils at 163167 C./15 mm.; and aethylsuberonitn'le boils at 184186 C./15 mm.
Reduction of 82 parts of a-ethylsuberonitrile in liquid ammonia over Raney nickel gave 60 parts of the C diamine, Z-ethyl-1,8-diaminooctane. The boiling point was 138-142 C./l0 mm., and the melting point was 26- 27 C. The diamine dihydrochloride melted at 160- 161 C.
Reduction of liquid ammonia C diamine,
82 parts of a,a'-diethyladiponitrile in over Raney nickel gave 60 parts of the 2,5-diethyl-1,6-diaminohexane, boiling at The diamine dihydrochloride parts of 2-ethvl-1,8diisocyanooctane; B. P. 110-112 C. at 0.1 mm. Hg; 94.6% yield. A sample of this cornpound was converted to the dimethyl urethane (51.5-53 C.) and as such gave the following analyses: Calculated for C H O N -C, 58.3; H, 9.78; N, 9.71; found-C, 58.4; H, 9.77; N, 9.80.
EXAMPLE VI The dihydrochloride of 2,5-diethyl-1,6-diaminohexane (24.5 parts) was suspended in 400 parts of dry xylene and raised to reflux temperature. A slow stream of phosgene was passed through the stirred suspension for 5 hours, during which time the reaction mixture became homogeneous. The preparation was distilled at atmospheric pressure to remove xylene and at 2 mm. pressure at which the 2,5-diethyl-1,6-diisocyanohexane was obtained as a water white liquid (B. P. 95-96 C.) in 55% yield, 11.3 gms.
Analysis.-Calculated for C H N O C, 64.27%; H, 8.98%; N, 12.48%. Found: C, 64.57%; H, 9.03%; N, 12.23%.
Table I below summarizes the data obtained from the procedures for preparation of diisocyanates as described in the above examples.
Table I PREPARATION OF DIISOCYANA TES While there are above disclosed but a limited number of embodiments of the process and examples of the compounds of the invention herein presented, it is possible to produce still other embodiments without departing from the inventive concept herein disclosed, and it is desired therefore that only such limitations be imposed on the appended claims as are stated therein.
What is claimed is:
1. The method of preparing saturated aliphatic C diisocyanates in which the isocyano (NCO) groups are separated by at least 4 carbon atoms, which includes the steps of dimerizing butadiene in the presence of sodium in finely dispersed form in an active ether diluent and in the presence of at least one dimerization activator, immediately carbonating the resulting organornetallic diene intermediate, neutralizing the resulting dialkali metal salts of dicarboxylic acids to obtain the free diacids, hydrogenating the unsaturated diacids, reacting the saturated diacids with at least one ammonia releasing agent to obtain the diamides, treating the diamides with alkaline hypohalite to give the diamines, and reacting the diamines with phosgene to obtain the C diisocyanates.
2. The method of preparing saturated aliphatic C diisocyanates in which the isocyano (NCO) groups are separated by at least 6 carbon atoms, which includes the steps of dimerizing butadiene in the presence of sodium in finely dispersed form in an active ether diluent and in the presence of at least one dimerization activator, immediately carbonating the resulting organometallic diene intermediate, neutralizing the resulting dialkali metal salts of dicarboxylic acids to obtain the free diacids, hydrogenating the unsaturated diacids, heating the saturated diacids with at least one ammonia releasing agent to obtain the dinitriles, hydrogenating the resulting dinitriles to diamines, and reacting the diamines with phosgene to obtain the C diisocyanates.
References Cited in the file of this patent UNITED STATES PATENTS 2,132,849 Greenwalt et a1. Oct. 11, 1938 2,200,282 Lazier May 14, 1940 Temp., B. P. at Yield,
C. 1-2 mm., Percent 2,319,057 Hanford May 11, 1943 2,352,461 Walker June 27, 1944 2,394,597 Dickey et a1 Feb. 12, 1946 2,584,527 Albisetti et a1. Feb. 5, 1952 2,716,662 Cohen et al Aug. 30, 1955 OTHER REFERENCES Karrer: Organic Chemistry, 4th English edition 1950), p. 130.
Claims (1)
1. THE METHOD OF PREPARING SATURATED ALIPHATIC C8 DIISOCYANATES IN WHICH THE ISOCYANO (-NCO) GROUPS ARE SEPARATED BY AT LEAST 4 CARBON ATOMS, WHICH INCLUDES STEPS OF DIMERIZING BUTADIENE IN THE PRESENCE OF SODIUM IN FINELY DISPERSED FORM IN AN ACTIVE ETHER DIULENT AND IN THE PRESENCE OF AT LEAST ONE DIMERIZATION ACTIVATOR, IMMEDIATELY CARBONATING THE RESULTING ORGANOMETALLIC DIENE INTERMEDIATE, NEUTRALIZING THE RESULTING DIALKALI METAL SALTS OF DICARBOXYLIC ACIDS TO OBTAIN THE FREE DIACIDS, HYDROGENATING THE UNSATURATED DIACIDS, REACTING THE SATURATED DIACIDS WITH AT LEAST ONE AMMONIA RELEASING AGENT TO OBTAIN THE DIAMIDES, TREATING THE DIAMIDES, WITH ALKALINE HYPOHALITE TO GIVE THE DIAMINES, THE REACTING THE DIAMINES WITH PHOSGENE TO OBTAIN THE C8 DIISOCYANATES.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US475293A US2865940A (en) | 1954-12-14 | 1954-12-14 | Process for preparing saturated aliphatic diisocyanates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US475293A US2865940A (en) | 1954-12-14 | 1954-12-14 | Process for preparing saturated aliphatic diisocyanates |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2865940A true US2865940A (en) | 1958-12-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US475293A Expired - Lifetime US2865940A (en) | 1954-12-14 | 1954-12-14 | Process for preparing saturated aliphatic diisocyanates |
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Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3084182A (en) * | 1960-05-09 | 1963-04-02 | Mobay Chemical Corp | Blocked isocyanates from still residues |
| US3180852A (en) * | 1959-05-08 | 1965-04-27 | Bayer Ag | Polyurethane plastics |
| US3203931A (en) * | 1959-08-05 | 1965-08-31 | Gen Tire & Rubber Co | Urethanes made from 4-substituted toluene dhsocyanate and a polyether or polyester |
| US3232973A (en) * | 1959-09-22 | 1966-02-01 | Bayer Ag | 1,2-di(isocyanatomethyl)cyclobutane |
| US3236813A (en) * | 1959-05-29 | 1966-02-22 | Bayer Ag | Polyurethanes from masked isocyanates |
| US3281378A (en) * | 1963-06-06 | 1966-10-25 | Merck & Co Inc | Diisocyanato substituted aliphatic carboxylic acid ester urethane reaction products |
| US3465023A (en) * | 1965-12-07 | 1969-09-02 | Gen Mills Inc | Preparation of nonaromatic polyisocyanates |
| US3624122A (en) * | 1966-06-24 | 1971-11-30 | Gen Mills Inc | Alicyclic diisocyanates |
| US3625986A (en) * | 1967-12-28 | 1971-12-07 | Nat Distillers Chem Corp | Bis 1, 1 isocyanatoalkyl cycloalkanes |
| US3668171A (en) * | 1971-01-11 | 1972-06-06 | Foster Grant Co Inc | Nylon compositions containing diisocyanate mold release agents |
| US3725357A (en) * | 1971-12-29 | 1973-04-03 | Gen Tire & Rubber Co | Temperature stable flexible isocyanate-terminated polymers and polyisocyanurate polymers therefrom |
| FR2340305A1 (en) * | 1976-02-07 | 1977-09-02 | Bayer Ag | DIISOCYANATES, THEIR PREPARATION AND THEIR USES AS SYNTHETIC COMPONENTS FOR THE PREPARATION OF POLYURETHANNES |
| US4131604A (en) * | 1977-11-23 | 1978-12-26 | Thermo Electron Corporation | Polyurethane elastomer for heart assist devices |
| US4304731A (en) * | 1980-12-30 | 1981-12-08 | Toray Industries, Incorporated | Method for producing an aliphatic triisocyanate |
| US4314048A (en) * | 1980-03-11 | 1982-02-02 | Asahi Kasei Kogyo Kabushiki Kaisha | Aliphatic triisocyanate, a method for preparing it and the preparation of polyurethane resins therewith |
| US4410597A (en) * | 1978-12-28 | 1983-10-18 | Toray Industries, Inc. | Polyurethane resins and polyurethane resin coating compositions |
| FR2560596A1 (en) * | 1984-03-02 | 1985-09-06 | Atochem | 1,1-DECANE DIISOCYANATES AND METHODS OF MAKING THE SAME |
| EP0241690A2 (en) * | 1986-03-13 | 1987-10-21 | Bayer Ag | Aliphatic diisocyanates and their use for the preparation of polyurethane polymers |
| US5554787A (en) * | 1990-03-30 | 1996-09-10 | Basf Aktiengesellschaft | 2,2-dialkylpentane 1,5-diisocyanates, 2,2-dialkylpentane 1,5-diurethanes and 2,2-dialkylpentane 1,5-dicarbamoyl chlorides, and their preparation and use |
| US20050010069A1 (en) * | 2001-12-11 | 2005-01-13 | Fitchett Colin Stanley | Oil ozonolysis |
| JP2019085350A (en) * | 2017-11-02 | 2019-06-06 | 三菱瓦斯化学株式会社 | Method for producing aliphatic diamine |
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| US2200282A (en) * | 1938-03-17 | 1940-05-14 | Du Pont | Vapor phase catalytic hydrogenation of adiponitrile |
| US2319057A (en) * | 1938-03-15 | 1943-05-11 | Du Pont | Preparation of long chain organic isocyanates |
| US2352461A (en) * | 1942-02-25 | 1944-06-27 | Du Pont | High molecular weight unsaturated organic acids and process of preparing them |
| US2394597A (en) * | 1942-07-09 | 1946-02-12 | Eastman Kodak Co | Preparation of organic dhsocyanates |
| US2584527A (en) * | 1949-11-02 | 1952-02-05 | Du Pont | Unsaturated dicarboxylic acids and esters and their preparation |
| US2716662A (en) * | 1952-01-24 | 1955-08-30 | Exxon Research Engineering Co | Polycyclic dibasic acids |
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| US2132849A (en) * | 1936-12-02 | 1938-10-11 | Du Pont | Process for preparing aliphatic dinitriles |
| US2319057A (en) * | 1938-03-15 | 1943-05-11 | Du Pont | Preparation of long chain organic isocyanates |
| US2200282A (en) * | 1938-03-17 | 1940-05-14 | Du Pont | Vapor phase catalytic hydrogenation of adiponitrile |
| US2352461A (en) * | 1942-02-25 | 1944-06-27 | Du Pont | High molecular weight unsaturated organic acids and process of preparing them |
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| US2584527A (en) * | 1949-11-02 | 1952-02-05 | Du Pont | Unsaturated dicarboxylic acids and esters and their preparation |
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Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3180852A (en) * | 1959-05-08 | 1965-04-27 | Bayer Ag | Polyurethane plastics |
| US3236813A (en) * | 1959-05-29 | 1966-02-22 | Bayer Ag | Polyurethanes from masked isocyanates |
| US3203931A (en) * | 1959-08-05 | 1965-08-31 | Gen Tire & Rubber Co | Urethanes made from 4-substituted toluene dhsocyanate and a polyether or polyester |
| US3232973A (en) * | 1959-09-22 | 1966-02-01 | Bayer Ag | 1,2-di(isocyanatomethyl)cyclobutane |
| US3084182A (en) * | 1960-05-09 | 1963-04-02 | Mobay Chemical Corp | Blocked isocyanates from still residues |
| US3281378A (en) * | 1963-06-06 | 1966-10-25 | Merck & Co Inc | Diisocyanato substituted aliphatic carboxylic acid ester urethane reaction products |
| US3465023A (en) * | 1965-12-07 | 1969-09-02 | Gen Mills Inc | Preparation of nonaromatic polyisocyanates |
| US3624122A (en) * | 1966-06-24 | 1971-11-30 | Gen Mills Inc | Alicyclic diisocyanates |
| US3625986A (en) * | 1967-12-28 | 1971-12-07 | Nat Distillers Chem Corp | Bis 1, 1 isocyanatoalkyl cycloalkanes |
| US3668171A (en) * | 1971-01-11 | 1972-06-06 | Foster Grant Co Inc | Nylon compositions containing diisocyanate mold release agents |
| US3725357A (en) * | 1971-12-29 | 1973-04-03 | Gen Tire & Rubber Co | Temperature stable flexible isocyanate-terminated polymers and polyisocyanurate polymers therefrom |
| US4107199A (en) * | 1976-02-07 | 1978-08-15 | Bayer Aktiengesellschaft | Bis(isocyanatopropyl) arylacetonitriles |
| FR2340305A1 (en) * | 1976-02-07 | 1977-09-02 | Bayer Ag | DIISOCYANATES, THEIR PREPARATION AND THEIR USES AS SYNTHETIC COMPONENTS FOR THE PREPARATION OF POLYURETHANNES |
| US4131604A (en) * | 1977-11-23 | 1978-12-26 | Thermo Electron Corporation | Polyurethane elastomer for heart assist devices |
| US4410597A (en) * | 1978-12-28 | 1983-10-18 | Toray Industries, Inc. | Polyurethane resins and polyurethane resin coating compositions |
| US4314048A (en) * | 1980-03-11 | 1982-02-02 | Asahi Kasei Kogyo Kabushiki Kaisha | Aliphatic triisocyanate, a method for preparing it and the preparation of polyurethane resins therewith |
| US4304731A (en) * | 1980-12-30 | 1981-12-08 | Toray Industries, Incorporated | Method for producing an aliphatic triisocyanate |
| EP0157661A1 (en) * | 1984-03-02 | 1985-10-09 | Elf Atochem S.A. | Diisocyanates 1-10 decane and process for their preparation |
| FR2560596A1 (en) * | 1984-03-02 | 1985-09-06 | Atochem | 1,1-DECANE DIISOCYANATES AND METHODS OF MAKING THE SAME |
| US4574059A (en) * | 1984-03-02 | 1986-03-04 | Atochem | Decane-1,10-diisocyanates and methods of making the same |
| EP0241690A2 (en) * | 1986-03-13 | 1987-10-21 | Bayer Ag | Aliphatic diisocyanates and their use for the preparation of polyurethane polymers |
| EP0241690A3 (en) * | 1986-03-13 | 1989-06-28 | Bayer Ag | Aliphatic diisocyanates and their use for the preparation of polyurethane polymers |
| US5554787A (en) * | 1990-03-30 | 1996-09-10 | Basf Aktiengesellschaft | 2,2-dialkylpentane 1,5-diisocyanates, 2,2-dialkylpentane 1,5-diurethanes and 2,2-dialkylpentane 1,5-dicarbamoyl chlorides, and their preparation and use |
| US20050010069A1 (en) * | 2001-12-11 | 2005-01-13 | Fitchett Colin Stanley | Oil ozonolysis |
| JP2019085350A (en) * | 2017-11-02 | 2019-06-06 | 三菱瓦斯化学株式会社 | Method for producing aliphatic diamine |
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